Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
  • C08G63/66—Polyesters containing oxygen in the form of ether groups
  • C08G63/668—Polyesters containing oxygen in the form of ether groups derived from polycarboxylic acids and polyhydroxy compounds
  • C08G63/672—Dicarboxylic acids and dihydroxy compounds
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L95/00—Compositions of bituminous materials, e.g. asphalt, tar, pitch
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J11/00—Recovery or working-up of waste materials
  • C08J11/04—Recovery or working-up of waste materials of polymers
  • C08J11/10—Recovery or working-up of waste materials of polymers by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation
  • C08J11/18—Recovery or working-up of waste materials of polymers by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation by treatment with organic material
  • C08J11/22—Recovery or working-up of waste materials of polymers by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation by treatment with organic material by treatment with organic oxygen-containing compounds
  • C08J11/24—Recovery or working-up of waste materials of polymers by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation by treatment with organic material by treatment with organic oxygen-containing compounds containing hydroxyl groups
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J3/00—Processes of treating or compounding macromolecular substances
  • C08J3/005—Processes for mixing polymers
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J3/00—Processes of treating or compounding macromolecular substances
  • C08J3/20—Compounding polymers with additives, e.g. colouring
  • C08J3/203—Solid polymers with solid and/or liquid additives
• • E—FIXED CONSTRUCTIONS
  • E01—CONSTRUCTION OF ROADS, RAILWAYS, OR BRIDGES
  • E01C—CONSTRUCTION OF, OR SURFACES FOR, ROADS, SPORTS GROUNDS, OR THE LIKE; MACHINES OR AUXILIARY TOOLS FOR CONSTRUCTION OR REPAIR
  • E01C7/00—Coherent pavings made in situ
  • E01C7/08—Coherent pavings made in situ made of road-metal and binders
  • E01C7/18—Coherent pavings made in situ made of road-metal and binders of road-metal and bituminous binders
  • E01C7/26—Coherent pavings made in situ made of road-metal and binders of road-metal and bituminous binders mixed with other materials, e.g. cement, rubber, leather, fibre
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2367/00—Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
  • C08J2367/02—Polyesters derived from dicarboxylic acids and dihydroxy compounds
  • C08J2367/03—Polyesters derived from dicarboxylic acids and dihydroxy compounds the dicarboxylic acids and dihydroxy compounds having the hydroxy and the carboxyl groups directly linked to aromatic rings
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2395/00—Bituminous materials, e.g. asphalt, tar or pitch
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2467/00—Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
  • C08J2467/02—Polyesters derived from dicarboxylic acids and dihydroxy compounds
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2467/00—Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
  • C08J2467/02—Polyesters derived from dicarboxylic acids and dihydroxy compounds
  • C08J2467/03—Polyesters derived from dicarboxylic acids and dihydroxy compounds the dicarboxylic acids and dihydroxy compounds having the hydroxy and the carboxyl groups directly linked to aromatic rings
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2495/00—Bituminous materials, e.g. asphalt, tar or pitch
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
  • Y02W30/00—Technologies for solid waste management
  • Y02W30/50—Reuse, recycling or recovery technologies
  • Y02W30/62—Plastics recycling; Rubber recycling

Definitions

• the present invention relates to an asphalt composition, an asphalt mixture, and methods of producing the same, and also relates to a method of paving a road.
• Asphalt pavement using an asphalt composition has been frequently performed for paving driveways, parking spaces, cargo yards, sidewalks, etc., because of relatively easy construction and a short period of time from beginning of paving works to traffic start.
• a road surface is formed of an asphalt mixture containing aggregates bonded with each other through asphalt, and hence, the paved roads exhibit good hardness and durability.
• JP 2006-096799 A discloses, for the purpose of providing a high-value plastic composition having desired characteristics for a pavement material in which waste PET can be treated in a large amount at as low a cost as possible, a method of producing a plastic composition for a pavement material in which waste PET and one or two or more polyhydric alcohols and/or a saccharide are subjected to transesterification in the presence of a catalyst to obtain a plastic composition for a pavement material.
• PTL 2 JP 2017/125421 A discloses, as an asphalt composition for road pavement excellent in dry strength, water immersion strength, and petroleum immersion strength, an asphalt composition for road pavement, containing an asphalt, a polyester resin, and an aggregate, the polyester resin being a polyester having a structural unit derived from an alcohol component containing 65% by mole or more of an alkylene oxide adduct of bisphenol A and a structural unit derived from a carboxylic acid component containing 50% by mole or more of one or more selected from the group consisting of terephthalic acid and isophthalic acid, the asphalt composition having a softening point of 95° C. or higher and 130° C. or lower, a hydroxyl value of 20 mgKOH/g or more and 50 mgKOH/g or less, and a ratio of the polyester resin of 5 parts by mass or more and 50 parts by mass or less relative to 100 parts by mass of the asphalt.
• the polyester resin being a polyester having a structural unit derived from an alcohol component containing 65% by mole or more
• the present invention relates to an asphalt composition containing an asphalt and a polyester, the polyester being a polycondensate of a polyethylene terephthalate, an alcohol, and a carboxylic acid compound, the alcohol containing an alkylene oxide adduct of bisphenol A.
• the present invention relates to an asphalt composition that is excellent in the storage stability and that can suppress rutting of a paved surface after laying, an asphalt mixture, and methods of producing the same.
• the present invention relates to the following [1] to [4].
• Step 1 a step of subjecting a polyethylene terephthalate, an alcohol component containing an alkylene oxide adduct of bisphenol A, and a carboxylic acid component to a polycondensation reaction in the presence of an esterification catalyst to obtain a polyester, and
• Step 2 a step of mixing an asphalt with the polyester obtained in the Step 1.
• Step 1 a step of subjecting a polyethylene terephthalate, an alcohol component containing an alkylene oxide adduct of bisphenol A, and a carboxylic acid component to a polycondensation reaction in the presence of an esterification catalyst to obtain a polyester, and
• Step 2 a step of mixing a heated aggregate, an asphalt, and the polyester obtained in the Step 1.
• an asphalt composition that is excellent in the storage stability and that can suppress rutting of a paved surface after laying, an asphalt mixture, and methods of producing the same.
• the asphalt composition of the present invention (hereinafter also referred to simply as “the asphalt composition”) contains an asphalt and a polyester.
• the polyester is a polycondensate of a polyethylene terephthalate, an alcohol, and a carboxylic acid compound, and the alcohol contains an alkylene oxide adduct of bisphenol A.
• an asphalt composition that is excellent in the storage stability and that can suppress rutting of a paved surface after laying can be obtained. Furthermore, by applying this technology, an asphalt mixture and a method for producing an asphalt mixture can be provided.
• PET polyethylene terephthalate
• the melting point of the PET is a relatively high temperature of 260° C.
• the PET is present in paving as masses that remain to have original particle diameters thereof, which is a factor of reduction in the rutting resistance of the asphalt mixture.
• the polyester used in the present invention is a polycondensate of PET, an alcohol, and a carboxylic acid compound.
• a transesterification reaction occurs by subjecting PET to polycondensation with an alcohol component and a carboxylic acid component, and thus a structural unit of PET is incorporated into an alcohol component-derived structural unit and a carboxylic acid component-derived structural unit in the polyester.
• the alcohol component contains an alkylene oxide adduct of bisphenol A. By containing a hydrophobic alkylene oxide adduct of bisphenol A, the polyester can be dispersed finely in a hydrophobic asphalt.
• Rutting is the unevenness generated continuously in the longitudinal direction of a road running portion due to flowage of an asphalt layer forming a paved surface at a high temperature, for example, in summer. Rutting corelates with the plastic flow resistance of an asphalt composition which functions as a binder in asphalt pavement, and can be evaluated by the G*/sin ⁇ of the asphalt composition (binder) according to the SUPERPAVE specification of binder (Japan Road Association, Extra Issue of Handbook for Method of Pavement Test, 1996).
• G* indicates the complex modulus of elasticity and G* and sin ⁇ are measured with a rheometer.
• the plastic flow resistance is larger, and thus, the asphalt composition is then evaluated as being capable of providing asphalt pavement excellent in the rutting resistance.
• a “binder mixture” means a mixture containing an asphalt and a thermoplastic elastomer, and for example, it has a concept including an asphalt modified with a thermoplastic elastomer as mentioned later (hereinafter also referred to as “modified asphalt”).
• an “alcohol component-derived structural unit” means a structure resulting from eliminating a hydrogen atom from a hydroxy group of the alcohol component
• a “carboxylic acid component-derived structural unit” means a structure resulting from eliminating a hydroxy group from a carboxy group of the carboxylic acid component.
• a “carboxylic acid compound” has a concept including not only a carboxylic acid but also an anhydride which is decomposed during the reaction to form an acid and an alkyl ester of a carboxylic acid (for example, the number of carbon atoms of the alkyl group is 1 or more and 3 or less).
• the carboxylic acid compound is an alkyl ester of a carboxylic acid
• the number of carbon atoms of the alkyl group that is an alcohol residue of the ester is not included in the number of carbon atoms of the carboxylic acid compound.
• the asphalt composition of the present invention contains an asphalt.
• a modified asphalt As the asphalt, various asphalts can be used.
• a modified asphalt is exemplified.
• the modified asphalt include blown asphalt; and an asphalt modified with a polymer material, such as a thermoplastic elastomer or a thermoplastic resin.
• Straight asphalt means a residual bituminous substance obtained by treating crude petroleum with an atmospheric distillation apparatus, a vacuum distillation apparatus, or the like.
• Blown asphalt means an asphalt obtained by heating a mixture of straight asphalt and heavy oil, then blowing the air into the mixture to oxidize them. From the viewpoint of the rutting resistance, a modified asphalt is preferred, and from the viewpoint of versatility, straight asphalt is preferred.
• phalt includes bitumen defined in the German industry standard DIN EN 12597. “Asphalt” and “bitumen” can be interchangeably used.
• the asphaltene content in the asphalt is preferably 10% by mass or more, more preferably 15% by mass or more, and preferably 30% by mass or less, more preferably 25% by mass or less, further preferably 20% by mass or less, in 100% by mass of the asphalt.
• the asphaltene content in the asphalt is a value measured by the Standard of the Japan Petroleum Institute, JPI-5S-22-83 “Fractional Analysis for Asphaltic Bitumen by Column Chromatography”.
• the asphalt composition preferably contains a thermoplastic elastomer.
• the asphalt and the thermoplastic elastomer are preferably used as a binder mixture which is a mixture thereof.
• An example of the binder mixture is a straight asphalt modified with a thermoplastic elastomer (modified asphalt).
• thermoplastic elastomer for example, at least one selected from the group consisting of a styrene/butadiene block copolymer (hereinafter also referred to simply as “SB”), a styrene/butadiene/styrene block copolymer (hereinafter also referred to simply as “SBS”), a styrene/butadiene random copolymer (hereinafter also referred to simply as “SBR”), a styrene/isoprene block copolymer (hereinafter also referred to simply as “SI”), a styrene/isoprene/styrene block copolymer (hereinafter also referred to simply as “SIS”), a styrene/isoprene random copolymer (hereinafter also referred to simply as “SIR”), an ethylene/vinyl acetate copolymer, and an ethylene/(vin
• thermoplastic elastomers from the viewpoint of enhancing rutting resistance, at least one selected from the group consisting of a styrene/butadiene block copolymer, a styrene/butadiene/styrene block copolymer, a styrene/butadiene random copolymer, a styrene/isoprene block copolymer, a styrene/isoprene/styrene block copolymer, and a styrene/isoprene random copolymer is preferred; and at least one selected from the group consisting of a styrene/butadiene random copolymer and a styrene/butadiene/styrene block copolymer is more preferred.
• the content of the thermoplastic elastomer in the asphalt composition is preferably 0.1% by mass or more, more preferably 0.5% by mass or more, further preferably 1% by mass or more, furthermore preferably 2% by mass or more, and preferably 30% by mass or less, more preferably 20% by mass or less, further preferably 10% by mass or less, furthermore preferably 5% by mass or less, in 100% by mass of the asphalt composition.
• the content of the thermoplastic elastomer in the asphalt composition is preferably 0.1% by mass or more, more preferably 0.5% by mass or more, further preferably 1% by mass or more, furthermore preferably 2% by mass or more, and preferably 30% by mass or less, more preferably 20% by mass or less, further preferably 10% by mass or less, furthermore preferably 5% by mass or less, relative to 100% by mass of the asphalt.
• the content of the asphalt in the asphalt composition is, from the viewpoint of the rutting resistance and the viewpoint of exhibiting the asphalt performance, preferably 60% by mass or more, more preferably 70% by mass or more, further preferably 75% by mass or more, furthermore preferably 80% by mass or more, and from the viewpoint of improving rutting, preferably 98% by mass or less, more preferably 97% by mass or less, further preferably 96% by mass or less, in 100% by mass of the asphalt composition.
• the asphalt composition of the present invention contains a polyester.
• the polyester is a polycondensate of a polyethylene terephthalate, an alcohol, and a carboxylic acid compound, and the alcohol contains an alkylene oxide adduct of bisphenol A.
• the alcohol component contains an alkylene oxide adduct of bisphenol A, preferably contains an alkylene oxide adduct of bisphenol A represented by the following formula (I).
• OR 1 and R 1 O is an alkylene oxide
• R 1 is an alkylene group having 2 or 3 carbon atoms
• x and y represent a positive number indicating the average number of moles of the alkylene oxide added
• the sum of x and y is preferably 1 or more, more preferably 1.5 or more, and preferably 16 or less, more preferably 8 or less, further preferably 4 or less.
• Examples of the alkylene oxide adduct of bisphenol A represented by the formula (I) include a propylene oxide adduct of bisphenol A [2,2-bis(4-hydroxyphenyl)propane] and an ethylene oxide adduct of bisphenol A.
• One of the alkylene oxide adducts of bisphenol A can be used alone or two or more thereof can be used in combination.
• the amount of the alkylene oxide adduct of bisphenol A used is preferably 80% by mole or more, more preferably 90% by mole or more, and is 100% by mole or less, in 100% by mole of the alcohol component in the polyester.
• the alcohol component may contain an alcohol component other than the alkylene oxide adduct of bisphenol A.
• examples thereof include an aliphatic diol, an aromatic diol (excluding an alkylene oxide adduct of bisphenol A), and a trihydric or higher polyhydric alcohol.
• One of the alcohol components can be used alone or two or more thereof can be used in combination.
• Examples of the aliphatic diol include ethylene glycol, 1,2-propanediol, 1,3-propanediol, 1,3-butanediol, 1,4-butanediol, 1,4-butenediol, 1,5-pentanediol, 1,6-hexanediol, neopentyl glycol, 1,10-decanediol, and 1,12-dodecanediol.
• the trihydric or higher polyhydric alcohol is, for example, a trihydric alcohol.
• An example of the trihydric or higher polyhydric alcohol is glycerol.
• carboxylic acid component examples include an aliphatic dicarboxylic acid compound, an aromatic dicarboxylic acid compound, and a tribasic or higher and hexabasic or lower polybasic carboxylic acid compound.
• carboxylic acid components can be used alone or two or more thereof can be used in combination.
• the number of carbon atoms in the main chain of the aliphatic dicarboxylic acid is preferably 3 or more, more preferably 4 or more, and preferably 10 or less, more preferably 8 or less.
• Examples of the aliphatic dicarboxylic acid compound include fumaric acid, maleic acid, oxalic acid, malonic acid, citraconic acid, itaconic acid, glutaconic acid, succinic acid, adipic acid, suberic acid, azelaic acid, sebacic acid, dodecanedioic acid, and a succinic acid substituted with an alkyl group having 1 or more and 20 or less carbon atoms or an alkenyl group having 2 or more and 20 or less carbon atoms, and anhydrides or alkyl esters (for example, the number of carbon atoms of the alkyl group is 1 or more and 3 or less) thereof.
• substituted succinic acid examples include dodecylsuccinic acid, dodecenylsuccinic acid, and octenylsuccinic acid.
• aliphatic dicarboxylic acid compounds at least one selected from the group consisting of fumaric acid, maleic acid, and adipic acid is preferred, and adipic acid is more preferred.
• aromatic dicarboxylic acid compound examples include phthalic acid, terephthalic acid, isophthalic acid, and naphthalenedicarboxylic acid, and anhydrides or alkyl esters (for example, the number of carbon atoms of the alkyl group is 1 or more and 3 or less) thereof.
• aromatic dicarboxylic acid compounds from the viewpoint of achieving rutting resistance, isophthalic acid and terephthalic acid are preferred, and terephthalic acid is more preferred.
• the tribasic or higher and hexabasic or lower carboxylic acid is preferably a tribasic carboxylic acid.
• Examples of the tribasic or higher and hexabasic or lower carboxylic acid include trimellitic acid, 2,5,7-naphthalenetricarboxylic acid, pyromellitic acid, and acid anhydrides thereof.
• a polyvalent carboxylic acid is contained, from the viewpoint of controlling properties, a monohydric alcohol may be appropriately contained in the alcohol component, and a monobasic carboxylic acid compound may be appropriately contained in the carboxylic acid component.
• the content of the aliphatic dicarboxylic acid compound in the carboxylic acid component is preferably 1% by mole or more, more preferably 3% by mole or more, further preferably 5% by mole or more, and preferably 15% by mole or less, more preferably 10% by mole or less, in 100% by mole of the carboxylic acid component.
• the content of the aromatic dicarboxylic acid compound is preferably 60% by mole or more, more preferably 75% by mole or more, and preferably 100% by mole or less, more preferably 99% by mole or less, further preferably 95% by mole or less, furthermore preferably 90% by mole or less, in 100% by mole of the carboxylic acid component.
• a molar ratio of the carboxylic acid component-derived structural unit to the alcohol component-derived structural unit [(carboxylic acid component)/(alcohol component)] is preferably 0.7 or more, and more preferably 0.8 or more, further preferably 0.9 or more, and preferably 1.5 or less, more preferably 1.3 or less, further preferably 1.1 or less.
• the polyester used in the present invention contains a structural unit composed of ethylene glycol and terephthalic acid derived from a polyethylene terephthalate.
• the polyethylene terephthalate may contain, besides the structural unit composed of ethylene glycol and terephthalic acid, a small amount of butanediol, isophthalic acid, or other components.
• polyethylene terephthalate is widely used as a product, such as a bottle or a film
• a polyethylene terephthalate that is produced as a product and then discarded and recovered (hereinafter referred to as “recovered PET”) is preferably used in the present invention in terms of the environmental issue and the cost.
• the type and the like of the recovered polyethylene terephthalate is not particularly limited as long as it has a certain level of purity. It may contain a small amount of a plastic, such as polyethylene or polypropylene, as an impurity.
• a waste pouch container can be used as the recovered PET.
• the specific size of the recovered product used in the present invention is, from the viewpoint of the reaction efficiency, preferably 4 mm 2 or more and 15 mm 2 or less and the thickness thereof is preferably 3 mm or less.
• the molar ratio (B)/(E) of a structural unit (B) derived from the alkylene oxide adduct of bisphenol A to a structural unit (E) composed of ethylene glycol and terephthalic acid derived from the polyethylene terephthalate is, from the viewpoints of the storage stability and the rutting resistance, preferably 30/70 or more, more preferably 50/50 or more, further preferably 60/40 or more, and preferably 95/5 or less, more preferably 90/10 or less, further preferably 80/20 or less.
• the (B)/(E) is preferably 30/70 or more and 95/5 or less, more preferably 50/50 or more and 90/10 or less, further preferably 60/40 or more and 80/20 or less.
• the polyester used in the present invention may be a polyester modified to the extent that the characteristics are not substantially impaired.
• a specific example of the modified polyester is a polyester obtained by grafting or blocking a polyester with phenol, urethane, epoxy, or the like by a method described in JP 11-133668 A, JP 10-239903 A, JP 8-20636 A, or the like.
• a preferred example of the modified polyester is a urethane-modified polyester obtained by subjecting a polyester to urethane-extension with a polyisocyanate compound.
• the softening point of the polyester is preferably 90° C. or higher, more preferably 95° C. or higher, further preferably 100° C. or higher, and preferably 140° C. or lower, more preferably 130° C. or lower, further preferably 125° C. or lower, furthermore preferably 120° C. or lower, furthermore preferably 115° C. or lower.
• the acid value of the polyester is, from the viewpoint of promoting adsorption to the aggregate to enhance the rutting resistance, preferably 2 mgKOH/g or more, more preferably 3 mgKOH/g or more, further preferably 5 mgKOH/g or more, and from the viewpoint of increasing water resistance of the paved surface, is preferably 40 mgKOH/g or less, more preferably 30 mgKOH/g or less, further preferably 20 mgKOH/g or less.
• the hydroxyl value of the polyester is preferably 1 mgKOH/g or more, more preferably 2 mgKOH/g or more, further preferably 5 mgKOH/g or more, furthermore preferably 10 mgKOH/g or more, and preferably 70 mgKOH/g or less, more preferably 50 mgKOH/g or less, further preferably 30 mgKOH/g or less, furthermore preferably 26 mgKOH/g or less.
• the glass transition point of the polyester is preferably 30° C. or higher, more preferably 40° C. or higher, further preferably 50° C. or higher, and preferably 80° C. or lower, more preferably 70° C. or lower, further preferably 65° C. or lower.
• the softening point, the acid value, the hydroxyl value, and the glass transition point can be measured by methods described in the section of Examples.
• the softening point, the acid value, the hydroxyl value, and the glass transition point can be controlled by the raw material monomer composition, molecular weight, catalyst amount, or reaction conditions.
• a method of producing the polyester is not particularly limited, and, for example, the polyester can be produced by subjecting a polyethylene terephthalate, an alcohol component containing an alkylene oxide adduct of bisphenol A, and a carboxylic acid component to polycondensation.
• the temperature of the polycondensation reaction is not particularly limited, and from the viewpoint of the reactivity and the viewpoint of the monomer decomposition temperature, the temperature is preferably 210° C. or higher and 260° C. or lower.
• the amount of the polyethylene terephthalate present in the raw materials is preferably 4% by mass or more, more preferably 10% by mass or more, further preferably 13% by mass or more, and preferably 80% by mass or less, more preferably 70% by mass or less, further preferably 40% by mass or less, in 100% by mass of the total amount of the polyethylene terephthalate, the alcohol component, and the carboxylic acid component.
• the amount of polyethylene terephthalate present in the raw materials is preferably 4% by mass or more and 80% by mass or less, more preferably 10% by mass or more and 70% by mass or less, further preferably 13% by mass or more and 40% by mass or less, in 100% by mass of the total amount of the polyethylene terephthalate, the alcohol component, and the carboxylic acid component.
• the polyethylene terephthalate may be present at the beginning of the polycondensation reaction or may be added to the reaction system during the polycondensation reaction.
• the timing of addition of the polyethylene terephthalate is preferably a stage in which the reaction rate of the alcohol component and the carboxylic acid component is 10% or less, and more preferably a stage in which the reaction rate is 5% or less.
• the reaction rate refers to a value of [amount of reaction water generated (mol)/theoretical amount of water generated (mol) ⁇ 100].
• a tin(II) compound having no Sn-C bond such as tin(II) di(2-ethylhexanoate)
• the amount of the esterification catalyst used is preferably 0.01 parts by mass or more, more preferably 0.2 parts by mass or more, and preferably 3.0 parts by mass or less, more preferably 1.5 parts by mass or less, relative to 100 parts by mass of the total amount of the alcohol component, the carboxylic acid component, and the polyethylene terephthalate.
• a pyrogallol compound such as gallic acid
• the amount of the esterification promoter used is preferably 0.001 parts by mass or more, more preferably 0.005 parts by mass or more, further preferably 0.01 parts by mass or more, and preferably 0.50 parts by mass or less, more preferably 0.20 parts by mass or less, further preferably 0.10 parts by mass or less, relative to 100 parts by mass of the total amount of the alcohol component, the carboxylic acid component, and the polyethylene terephthalate.
• the content of the polyester relative to 100 parts by mass of the asphalt is preferably 0.5 parts by mass, more preferably 1 parts by mass or more, further preferably 3 parts by mass or more, furthermore preferably 5 parts by mass or more, and preferably 50 parts by mass or less, more preferably 30 parts by mass or less, further preferably 20 parts by mass or less, furthermore preferably 10 parts by mass or less.
• the ratio (P)/(A) of the mass proportion (P) of the structural unit of polyethylene terephthalate in the polyester to the asphaltene content (A) in the asphalt is preferably 0.15 or more, more preferably 0.2 or more, more preferably 0.5 or more, more preferably 0.8, and preferably 3.5 or less, more preferably 3 or less, more preferably 2.7 or less.
• the method of producing an asphalt composition of the present invention preferably includes a step of mixing an asphalt with the polyester described above.
• An asphalt composition is obtained by melting an asphalt with heat, adding the polyester thereto, and mixing the mixture by stirring with a generally used mixer until the components are uniformly dispersed.
• the generally used mixer include a homomixer, a dissolver, a paddle mixer, a ribbon mixer, a screw mixer, a planetary mixer, a vacuum reverse-flow mixer, a roll mill, and a twin screw extruder.
• the temperature in mixing the asphalt and the polyester is preferably 100° C. or higher, more preferably 130° C. or higher, further preferably 160° C. or higher, furthermore preferably 170° C. or higher, and preferably 230° C. or lower, more preferably 210° C. or lower, further preferably 200° C. or lower, furthermore preferably 190° C. or lower.
• the time of mixing the asphalt and the polyester is preferably 1 minute 0.1 hours or more, more preferably 0.5 hours or more, further preferably 1.0 hour or more, furthermore preferably 1.5 hours or more, and preferably 10 hours or less, more preferably 7 hours or less, further preferably 5 hours or less, furthermore preferably 3 hours or less.
• the ratio (P)/(A) of the mass proportion (P) of the structural unit of polyethylene terephthalate in the polyester to the asphaltene content (A) in the asphalt is preferably 0.15 or more, more preferably 0.2 or more, more preferably 0.5 or more, more preferably 0.8, and preferably 3.5 or less, more preferably 3 or less, more preferably 2.7 or less.
• a preferred aspect of the method of producing an asphalt composition includes a step of subjecting a polyethylene terephthalate, an alcohol component containing an alkylene oxide adduct of bisphenol A, and a carboxylic acid component to a polycondensation reaction in the presence of an esterification catalyst to obtain a polyester (Step 1), and a step of mixing an asphalt with the polyester (the polyester obtained in the Step 1) (Step 2).
• the polyethylene terephthalate is preferably a recovered polyethylene terephthalate.
• the method of producing an asphalt composition preferably includes a step of recovering a polyethylene terephthalate from a product (Step la), a step of subjecting the polyethylene terephthalate (the polyethylene terephthalate obtained in the Step la), an alcohol component containing an alkylene oxide adduct of bisphenol A, and a carboxylic acid component to a polycondensation reaction in the presence of an esterification catalyst to obtain a polyester (Step 2a), and a step of mixing an asphalt with the polyester (the polyester obtained in the Step 2a) (Step 3a).
• the asphalt composition may contain a dispersant.
• the dispersant is preferably a dispersant soluble in an asphalt and having affinity with the polyester.
• dispersant examples include a polymer dispersant and a surfactant, such as a polyoxyethylene alkylamine and an alkanolamine.
• polymer dispersant examples include a polyamide amine and a salt thereof, a polycarboxylic acid and a salt thereof, a high-molecular weight unsaturated acid ester, a modified polyurethane, a modified polyester, a modified poly(meth)acrylate, a (meth)acrylic copolymer, and a naphthalenesulfonic acid formalin condensate.
• These dispersants may be used alone or in combination of two or more thereof.
• the dispersant is preferably a polymer dispersant.
• the “polymer dispersant”, as used in the present invention means a dispersant having a weight average molecular weight of 1,000 or more. Although the weight average molecular weight also depends on the polymer species, it is preferably 2,000 or more, more preferably 4,000 or more, and preferably 80,000 or less, more preferably 40,000 or less.
• the dispersant preferably has a basic functional group.
• the basic functional group means a group such that a pKa of the conjugate acid is -3 or more.
• Examples of the basic functional group include an amino group, an imino group, and a quaternary ammonium group
• the base value of the dispersant is preferably 10 mgKOH/g or more, more preferably 20 mgKOH/g or more, further preferably 30 mgKOH/g or more, and preferably 150 mgKOH/g or less, more preferably 120 mgKOH/g or less, further preferably 100 mgKOH/g or less.
• the base value is measured by the method prescribed in JIS K7237:1995.
• Examples of a commercially available dispersant include “DISPER” Series “byk-101”, “byk-130”, “byk-161”, “byk-162”, “byk-170”, “byk-2020”, “byk-2164”, and “byk-LPN21324” (all of which are manufactured by BYK Additives & Instruments; “SOLSPERSE” Series “9000”, “11200”, “13240”, “13650”, “13940”, “17000”, “18000”, “24000”, “28000”, “32000”, “38500”, and “71000” (all of which are manufactured by Lubrizol Corp.); “AJISPER” Series “PB821”, “PB822”, “PB880”, and “PB881” (all of which are manufactured by Ajinomoto Fine-Techno Co., Inc.); “EFKA” Series “46”, “47”, “48”, “49”, “4010”, “4047”, “4050”, “4165”, and “5010” (all of which are manufactured by BASF SE
• the content of the dispersant is preferably 1 part by mass or more, more preferably 3 parts by mass or more, further preferably 4 parts by mass or more, and preferably 80 parts by mass or less, more preferably 60 parts by mass or less, further preferably 40 parts by mass or less, furthermore preferably 30 parts by mass or less, furthermore preferably 20 parts by mass or less, relative to 100 parts by mass of the polyester.
• the asphalt composition of the present invention is a binder composition, and is used for pavement after an aggregate is added to the asphalt composition to prepare an asphalt mixture.
• the asphalt composition of the present invention is suitable for pavement, in particular, for pavement of a road.
• the asphalt mixture of the present invention contains the asphalt composition described above and an aggregate. That is, the asphalt mixture contains an asphalt, a polyester, and an aggregate, and preferably contains an asphalt, a thermoplastic elastomer, a polyester, and an aggregate.
• the content of the asphalt composition in the asphalt mixture is preferably 2% by mass or more, more preferably 3% by mass or more, further preferably 4% by mass or more, and preferably 15% by mass or less, more preferably 10% by mass or less, further preferably 8% by mass or less, in 100% by mass of the asphalt mixture.
• any of crushed stone, cobble stone, gravel, sand, recycled aggregate, ceramic, and the like can be selected and used.
• any of a coarse aggregate having a particle diameter of 2.36 mm or more and a fine aggregate having a particle diameter of less than 2.36 mm can be used.
• Examples of the coarse aggregate include crushed stone having a particle diameter range of 2.36 mm or more and 4.75 mm or less, crushed stone having a particle diameter range of 4.75 mm or more and 12.5 mm or less, crushed stone having a particle diameter range of 12.5 mm or more and 19 mm or less, and crushed stone having a particle diameter range of 19 mm or more and 31.5 mm or less.
• the fine aggregate is preferably a fine aggregate having a particle diameter of 0.075 mm or more and less than 2.36 mm.
• Examples of the fine aggregate include river sand, hill sand, mountain sand, sea sand, crushed sand, fine sand, screenings, crushed stone dust, silica sand, artificial sand, glass cullet, molding sand, and recycled aggregate-crushed sand.
• the aforementioned particle diameter is a value prescribed in JIS 5001:1995.
• the fine aggregate may contain a filler having a particle diameter of less than 0.075 mm (for example, sand).
• a filler having a particle diameter of less than 0.075 mm for example, sand.
• the filler include sand, fly ash, calcium carbonate, and hydrated lime. Among them, from the viewpoint of enhancing the dry strength, calcium carbonate is preferred.
• the average particle diameter of the filler is preferably 0.001 mm or more, and preferably 0.05 mm or less, more preferably 0.03 mm or less, further preferably 0.02 mm or less.
• the average particle diameter of the filler can be measured by a laser diffraction particle size distribution analyzer.
• the average particle diameter means an average particle diameter of 50% cumulative volume.
• the average particle diameter of the filler is a value measured using a laser diffraction particle size distribution analyzer (LA-950, manufactured by HORIBA, Ltd.) under the following conditions.
• a mass ratio of the coarse aggregate to the fine aggregate is preferably 10/90 or more, more preferably 20/80 or more, further preferably 30/70 or more, and preferably 90/10 or less, more preferably 80/20 or less, further preferably 70/30 or less.
• the content of the aggregate is preferably 1,000 parts by mass or more, more preferably 1,200 parts by mass or more, further preferably 1,400 parts by mass or more, and preferably 3,000 parts by mass or less, more preferably 2,500 parts by mass or less, and further preferably 2,000 parts by mass or less, relative to 100 parts by mass of the asphalt composition.
• Suitable examples of blending in the asphalt mixture are as follows.
• a blending proportion of the asphalt is generally adopted according to an optimum asphalt amount obtained from “Formulation and Design of Asphalt Composition” as described in “Guideline for Pavement Design and Construction” published by Japan Road Association.
• the aforementioned optimum asphalt amount corresponds to the total amount of the asphalt, the thermoplastic elastomer, and the polyester. Accordingly, in general, the aforementioned optimum asphalt amount is preferably adopted as the total amount of the asphalt, the thermoplastic elastomer, and the polyester blended.
• the method of determining the amount is not to be limited to the method as described in “Guideline for Pavement Design and Construction”, and the amount may also be determined by any other methods.
• the method of producing an asphalt mixture of the present invention includes a step of subjecting a polyethylene terephthalate, an alcohol component containing an alkylene oxide adduct of bisphenol A, and an carboxylic acid component to a polycondensation reaction in the presence of an esterification catalyst to obtain a polyester (Step 1), and mixing a heated aggregate, an asphalt, and the polyester (the polyester obtained in the Step 1) (Step 2), and preferably includes a step of mixing a heated aggregate, an asphalt, a thermoplastic elastomer, and the polyester.
• a method of producing an asphalt mixture include conventional methods of producing an asphalt mixture called a plant mix method, a premix method, and the like.
• the methods are all a method in which an asphalt (and a thermoplastic elastomer as needed), and a polyester are added to a heated aggregate.
• the addition method include a premix method in which an asphalt (and a thermoplastic elastomer as needed), and a polyester are previously dissolved; and a plant mix method in which a modified asphalt having a thermoplastic elastomer dissolved in an asphalt is added, and then, a polyester is put therein.
• the premix method is preferred from the viewpoint of the rutting resistance.
• the temperature in previously mixing the asphalt and the polyester in the method of (iii) is, from the viewpoint of the rutting resistance, preferably a temperature higher than the softening point of the polyester, preferably 130° C. or higher, more preferably 150° C. or higher, further preferably 170° C. or higher, furthermore preferably 180° C. or higher, and from the viewpoint of preventing thermal degradation of the asphalt, preferably 230° C. or lower, more preferably 210° C. or lower, further preferably 200° C. or lower.
• the time of mixing is, for example, 10 minutes or more, preferably 30 minutes or more, more preferably 1 hour or more, more preferably 2 hours or more.
• the upper limit of the time is not particularly limited, and, for example, is about 5 hours.
• the temperature of the heated aggregate in the methods of (i) to (iii) is, from the viewpoint of the rutting resistance, a temperature higher than the softening point of the polyester, preferably 130° C. or higher, more preferably 150° C. or higher, further preferably 170° C. or higher, furthermore preferably 180° C. or higher, and from the viewpoint of preventing thermal decomposition of the asphalt, preferably 230° C. or lower, more preferably 210° C. or lower, further preferably 200° C. or lower.
• the temperature of mixing is preferably a temperature higher than the softening point of the polyester, preferably 130° C. or higher, more preferably 150° C. or higher, further preferably 170° C. or higher, furthermore preferably 180° C. or higher, and from the viewpoint of preventing thermal decomposition of the asphalt, preferably 230° C. or lower, more preferably 210° C. or lower, further preferably 200° C. or lower.
• the time of mixing in the step of mixing is, for example, 30 seconds or more, preferably 1 minute or more, more preferably 2 minutes or more, further preferably 5 minutes or more.
• the upper limit of the time is not particularly limited, and, for example, is about 30 minutes.
• the method of producing an asphalt mixture preferably includes, after the step of mixing, a step of keeping the obtained mixture at a temperature higher than the softening point of the polyester or higher.
• the mixture may be further mixed as long as the above-mentioned temperature or higher is kept.
• the temperature of mixing is preferably a temperature higher than the softening point of the polyester, preferably 130° C. or higher, more preferably 150° C. or higher, further preferably 170° C. or higher, furthermore preferably 180° C. or higher, and from the viewpoint of preventing thermal decomposition of the asphalt composition, is preferably 230° C. or lower, more preferably 210° C. or lower, further preferably 200° C. or lower.
• the time of keeping in the step of keeping is preferably 0.5 hours or more, more preferably 1 hour or more, further preferably 1.5 hours or more.
• the upper limit of the time is not particularly limited, and is, for example, about 5 hours.
• the polyethylene terephthalate is preferably a recovered polyethylene terephthalate.
• the method of producing an asphalt mixture includes a step of recovering a polyethylene terephthalate from a product (Step 1a), subjecting the polyethylene terephthalate (the polyethylene terephthalate obtained in the Step 1a), an alcohol component containing an alkylene oxide adduct of bisphenol A, and a carboxylic acid component to a polycondensation reaction in the presence of an esterification catalyst to obtain a polyester (Step 2a), and a step of mixing a heated aggregate, an asphalt, and the polyester (the polyester obtained in the Step 2a) (Step 3a).
• the asphalt mixture of the present invention is suitable for paving a road, and as described above, an asphalt mixture in which an aggregate is added to the asphalt composition is used for paving a road.
• the method of paving a road preferably includes laying the asphalt mixture on a road to form an asphalt pavement material layer.
• the method of paving a road includes a step of mixing an asphalt, the polyester, and an aggregate to obtain an asphalt mixture (Step 1), and a step of laying the asphalt mixture obtained in the Step 1 on a road to form an asphalt pavement material layer (Step 2).
• the asphalt pavement material layer is preferably a base course or a surface course.
• the asphalt mixture may be subjected to compaction laying by such a method using a known laying machine.
• a compaction temperature thereof is preferably a temperature higher than the softening point of the polyester, preferably 100° C. or higher, more preferably 120° C. or higher, further preferably 130° C. or higher, and preferably 200° C. or lower, more preferably 180° C. or lower.
• the present invention further discloses the following ⁇ 1> to ⁇ 7>.
• An asphalt composition containing an asphalt and a polyester the polyester being a polycondensate of a polyethylene terephthalate, an alcohol, and a carboxylic acid compound, the alcohol containing an alkylene oxide adduct of bisphenol A.
• the alcohol components, carboxylic acid component, and PET in the polyester of Table 1 were put in a 5-liter four-neck flask equipped with a thermometer, a stainless-steel stirrer bar, a flow-down condenser, and a nitrogen introducing tube, and tin(II) di(2-ethylhexanoate) and gallic acid in amounts shown in Table 1 were added under nitrogen atmosphere.
• the mixture was heated to 235° C. over 3 hours in a mantle heater, and was then kept at 235° C. for 5 hours.
• a binder mixture 2200 g of a modified asphalt type II (manufactured by TOA ROAD CORPORATION, asphaltene concentration in asphalt: 15% by mass) heated to 180° C. was put in a 3 L stainless steel container, and the asphalt was stirred at 100 rpm. Then, 110 g (5 parts by mass relative to 100 parts by mass of the asphalt) of a polyester resin (A1) was gradually added thereto, and the mixture was stirred at 300 rpm for 2 hours, thereby producing an asphalt composition (AS-1).
• a modified asphalt type II manufactured by TOA ROAD CORPORATION, asphaltene concentration in asphalt: 15% by mass
• Asphalt compositions (AS-2) to (AS-4) were produced in the same manner as in Example 1 except for changing the polyester resin (A1) in Example 1 to polyester resins (A2) to (A4), respectively.
• Asphalt mixtures (M-2) to (M-4) were obtained as a specimen in the same manner as in Example 1 except for changing 635 g of the asphalt composition (AS-1) in Example 1 to 635 g of asphalt compositions (AS-2) to (AS-4), respectively.
• An asphalt composition (AS-5) was obtained in the same manner as in Example 1 except for changing the amount of the polyester resin (A1) added in Example 1 to 550 g (25 parts by mass relative to 100 parts by mass of the asphalt).
• An asphalt mixture (M-5) was obtained as a specimen in the same manner as in Example 1 except for changing 635 g of the asphalt composition (AS-1) in Example 1 to 756 g of the asphalt composition (AS-5).
• An asphalt composition (AS-6) was obtained in the same manner as in Example 1 except for changing the asphalt in Example 1 to a straight asphalt (manufactured by TOA ROAD CORPORATION, asphaltene concentration in asphalt: 15% by mass).
• An asphalt mixture (M-6) was obtained as a specimen in the same manner as in Example 1 except for changing 635 g of the asphalt composition (AS-1) in Example 1 to 635 g of the asphalt composition (AS-6).
• An asphalt composition (AS-7) was obtained in the same manner as in Example 1 except for changing the asphalt in Example 1 to a modified asphalt “PG76-22” (manufactured by Ergon, Inc. in Texas, US, asphaltene concentration in asphalt: 22% by mass).
• An asphalt mixture (M-7) was obtained as a specimen in the same manner as in Example 1 except for changing 635 g of the asphalt composition (AS-1) in Example 1 to 635 g of the asphalt composition (AS-7).
• An asphalt composition (AS-8) was obtained in the same manner as in Example 3 except for changing the asphalt in Example 1 to a modified asphalt (manufactured by FESPA in Mexico, asphaltene concentration in asphalt: 28% by mass).
• An asphalt mixture (M-8) was obtained as a specimen in the same manner as in Example 1 except for changing 635 g of the asphalt composition (AS-1) in Example 1 to 635 g of the asphalt composition (AS-8).
• An asphalt mixture (M-9) was obtained as a specimen in the same manner as in Example 1 except for changing 635 g of the asphalt composition (AS-1) in Example 1 to 716 g of the asphalt composition (AS-1).
• An asphalt mixture (M-10) was obtained as a specimen in the same manner as in Example 1 except for changing 635 g of the asphalt composition (AS-1) in Example 1 to 520 g of the asphalt composition (AS-1).
• Example 1 the modified asphalt type II was used as it was without adding the polyester resin (A1).
• An asphalt mixture (M-A) was obtained as a specimen in the same manner as in Example 1 except for changing 635 g of the asphalt composition (AS-1) in Example 1 to 605 g of the modified asphalt type II.
• Asphalt compositions (AS-al) to (AS-a2) were obtained in the same manner as in Example 1 except for changing the polyester resin (A1) in Example 1 to the polyester resins (a1) to (a2), respectively.
• Asphalt mixtures (M-a1) to (M-a2) were obtained as a specimen in the same manner as in Example 1 except for changing 635 g of the asphalt composition (AS-1) in Example 1 to 635 g of asphalt compositions (AS-al) to (AS-a2), respectively.
• An asphalt composition (AS-a3) was produced in the same manner as in Example 1 except for changing the polyester resin (A1) in Example 1 to PET 1 (“RAMAPET L1”, manufactured by Indorama Ventures).
• An asphalt mixture (M-a3) was obtained as a specimen in the same manner as in Example 1 except for changing 635 g of the asphalt composition (AS-1) in Example 1 to 635 g of the asphalt composition (AS - a3).
• the specimen was immersed in hot water set at 60° C. in a thermostatic chamber of 60° C., and a wheel was reciprocated on the specimen using a wheel tracking tester (manufactured by Iwata Kogyosho K. K., load: 1370 N, frettage width: 47 mm, linear load: 291.5 N/cm) at a speed of 15 rpm, and the displacements after 1,250 passings and 2,500 passings were measured.
• Other measurement conditions were according to “B003 Wheel Tracking Test” described in “Handbook for Method of Assessment and Test for Pavement” published by Japan Road Association.
• Example 1 In Examples 1 to 5, 7 to 10 and Comparative Examples 1 to 4 in which a modified asphalt was used, hot water set at 60° C. was allowed to infiltrate into the specimen in a thermostatic chamber of 60° C., and the displacement after 2,500 tire passings was measured. In Example 6 in which a straight asphalt was used, hot water set at 50° C. was allowed to infiltrate into the specimen in a thermostatic chamber of 50° C., and the displacement after 1,250 tire passings was measured. The results are shown in Table 2.
• Comparative Example 2 in which a structural unit composed of ethylene glycol and terephthalic acid derived from polyethylene terephthalate is not contained, although rutting can be suppressed, the storage stability of the asphalt at a high temperature is poor.
• Comparative Example 4 in which polyethylene terephthalate was blended as it was and Comparative Example 3 in which a structural unit derived from an alkylene oxide adduct of bisphenol A was not contained, rutting cannot be sufficiently suppressed.
• an asphalt composition containing a specific polyester having a structural unit composed of ethylene glycol and terephthalic acid derived from polyethylene terephthalate and a structural unit derived from an alkylene oxide adduct of bisphenol A is excellent in the storage stability and rutting of a paved surface after laying can be further suppressed.

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